US8925353B2 - Process and system for fining glass - Google Patents

Process and system for fining glass Download PDF

Info

Publication number
US8925353B2
US8925353B2 US12/264,562 US26456208A US8925353B2 US 8925353 B2 US8925353 B2 US 8925353B2 US 26456208 A US26456208 A US 26456208A US 8925353 B2 US8925353 B2 US 8925353B2
Authority
US
United States
Prior art keywords
glass
making process
process according
wall portion
fining
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active, expires
Application number
US12/264,562
Other versions
US20090120133A1 (en
Inventor
Raymond Eugene Fraley
Paul Richard Grzesik
Lawrence Henry Kotacska
William Brashear Mattingly, III
James Patrick Murphy
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Corning Inc
Original Assignee
Corning Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Corning Inc filed Critical Corning Inc
Priority to US12/264,562 priority Critical patent/US8925353B2/en
Assigned to CORNING INCORPORATED reassignment CORNING INCORPORATED ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FRALEY, RAYMOND EUGENE, MATTINGLY, III, WILLIAM BRASHEAR, GRZESIK, PAUL RICHARD, KOTACSKA, LAWRENCE HENRY, MURPHY, JAMES PAT
Publication of US20090120133A1 publication Critical patent/US20090120133A1/en
Application granted granted Critical
Publication of US8925353B2 publication Critical patent/US8925353B2/en
Active legal-status Critical Current
Adjusted expiration legal-status Critical

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/225—Refining
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/42—Details of construction of furnace walls, e.g. to prevent corrosion; Use of materials for furnace walls
    • C03B5/43—Use of materials for furnace walls, e.g. fire-bricks
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00—Technologies relating to the processing of minerals
    • Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
    • Y02P40/57—Improving the yield, e-g- reduction of reject rates

Definitions

  • the present invention relates to process and system for fining molten glass.
  • the present invention relates to glass fining process and system comprising a metal fining vessel.
  • the present invention is useful, e.g., in the direct heated platinum fining system for making LCD glass substrate.
  • An exemplary process for manufacturing glass articles begins with the melting of raw feed materials, such as metal oxides, to form a molten glass.
  • the melting process not only results in the formation of glass, but also the formation of various unwanted by-products, including various gases such as oxygen, carbon dioxide, carbon monoxide, sulfur dioxide, sulfur trioxide, argon, nitrogen, and water. Unless removed, these gases can continue throughout the manufacturing process, ending up as small, sometimes microscopic gaseous inclusions or blisters in the finished glass article.
  • gaseous inclusions For some glass articles, the presence of small gaseous inclusions is not detrimental. However, for other articles of manufacture, gaseous inclusions as small as 50 ⁇ m in diameter are unacceptable.
  • One such article is the glass sheet used in the manufacture of display devices such as liquid crystal and organic light emitting diode displays. For such applications, the glass must have extraordinary clarity, pristine surfaces, and be essentially free of distortion and inclusions.
  • a fining agent or agents are typically added to the feed material.
  • the fining agent can be a multivalent oxide, such as As 2 O 3 .
  • As 2 O 3 is converted into As 2 O 5 during glass melting process.
  • the following reaction occurs: As 2 O 5 ⁇ As 2 O 3 +O 2 (gas)
  • the released oxygen forms gas bubbles in the molten glass, or melt.
  • the gas bubbles allow other dissolved gases to be collected and rise to the surface of the melt, where it is removed from the process.
  • the heating is typically performed in a high temperature fining vessel.
  • the fining temperatures for display-grade glasses can be as high as 1700° C. Temperatures this high require the use of specialized metals or alloys to prevent destruction of the vessel. Platinum or platinum alloys, such as platinum-rhodium are typically used. Platinum advantageously has a high melting temperature and does not easily dissolve in the glass. Nevertheless, at such high temperatures, the platinum or platinum alloy readily oxidizes. Therefore, steps must be taken to prevent contact between the hot platinum fining vessel and atmospheric oxygen. Other measures for reducing the oxidation of Pt during glass fining and delivery is highly desired as well.
  • the material forming the fining system such as one made with a metal or a metal alloy, has a maximal operating temperature. Therefore, it would be desirable to have a glass fining system which provides a high fining temperature to the molten glass without exceeding the highest operating temperature of the metal.
  • the present invention satisfies this need.
  • a first aspect of the present invention is a glass making process comprising a step of fining the molten glass in a fining vessel comprising a top wall portion not in direct contact with the molten glass, and a side wall portion in direct contact with the molten glass, wherein the top wall portion has a temperature T(top), the side wall portion has a temperature T(side), and T(top) ⁇ T(side) ⁇ 10° C.
  • the wall portions of the vessel comprises a metal.
  • the vessel is heated by passing an electric current through the wall portions.
  • the wall portions of the vessel comprise Pt.
  • T(side) ⁇ 1600° C. in certain embodiments T(side) ⁇ 1630° C., in certain embodiments T(side) ⁇ 1650° C., in certain embodiments T(side) ⁇ 1660° C., in certain embodiments T(side) ⁇ 1670° C., in certain embodiments T(side) ⁇ 1680° C., in certain embodiments T(side) ⁇ 1690° C., in certain embodiments T(side) ⁇ 1700° C.
  • the molten glass is a borosilicate glass, in certain embodiments an aluminoborosilicate glass.
  • the fining vessel is supported by a cradle in which the vessel is placed.
  • the fining vessel is enclosed by multiple layers of heat-insulating materials.
  • the fining vessel is enclosed by at least one layer of heat-insulating material rated for a working temperature of at least 1650° C.
  • the fining vessel is enclosed by at least one layer of fire board.
  • the side wall portion of the fining vessel is further differentially heated by supplemental heating, such as by passing a current through a Pt heating system or other direct metal heating system.
  • cooling fins or heat sinks are installed on the outside of the top wall portion of the fining vessel.
  • the top wall portion of the fining vessel has a larger thickness than the side wall portion.
  • the wall portions of the fining vessel comprises a metal, and the oxidation of the metal is reduced compared to where T(top) ⁇ T(side) ⁇ 30° C.
  • a second aspect of the present invention is a glass fining system comprising:
  • a metal vessel operable to allow a molten glass to fine therein, having a top wall portion which the molten glass essentially does not directly contact, and a side wall portion which the motel glass directly contact, during a glass fining process;
  • a first temperature sensor operable to sense the temperature of the top wall portion
  • a second temperature sensor operable to sense the temperature of the side wall portion
  • a current supply operable to supply an electric current through the wall portions of the metal vessel to heat the top wall portion and the side wall portion of the fining vessel;
  • the fining system is operable to maintain a difference between the temperature of the top wall portion, T(top), and the temperature of the side wall portion of the vessel, T(side), during the fining process, wherein T(top) ⁇ T(side) ⁇ 10° C.
  • the system further comprises a heating element operable to differentially heat the side wall portion of the metal vessel, such as a direct Pt heating system or other direct metal heating system.
  • a cooling fin or a heat sink is installed on the outside of the top wall portion of the metal vessel.
  • the top wall portion of the metal vessel has a higher thickness than the side wall portion.
  • the heat-insulating enclosure comprises at least one layer of fire board.
  • the metal vessel comprises Pt and/or an alloy thereof.
  • One or more embodiments of the present invention has one or more of the following advantages: (i) higher quality glass with fewer defects can be produced; (ii) oxidation of metal, such as precious metal, used in the construction of the fining vessel can be reduced, thus extending the life span of the system; (iii) superior thermal insulation of the system can be achieved; and (iv) optimal temperature uniformity of the molten glass can be obtained by using the present invention; (iv) significant capital savings can be realized; and (v) higher select of the glass produced can be obtained.
  • FIG. 1 is a schematic illustration of the cross-section of a metal fining vessel used in accordance with one embodiment of the present invention.
  • FIG. 2 is a schematic illustration of the cross-section of a fining system according to one embodiment of the present invention.
  • FIG. 3 is a diagram showing the oxidation (indicated by weight loss) of Pt—Rh alloy at various temperature and temperature gradient.
  • a typical glass fining system comprises a fining vessel where molten glass is contained for a certain period of residence time, where gas bubbles inside the molten glass are allowed to rise from inside the molten glass to the surface. All other conditions being equal, the lower the viscosity of the molten glass, the easier it is for the bubbles to form and rise in the melt. It is desirable that the molten glass in the fining vessel is heated to a sufficiently high temperature to allow for a sufficiently low glass viscosity. The highest temperature the glass melt can reach is determined in part by the material of the fining vessel. Take a fining system comprising a Pt fining vessel as an example. The temperature of the molten glass cannot exceed the melting temperature of Pt. Pure Pt has a melting point of 1768° C. The mechanical integrity of the Pt fining vessel can be seriously compromised if it is heated to a temperature close to its melting point.
  • differing parts of the fining vessel of a fining system may be subjected to differential heating during a fining process, due in part to the differing environment they are exposed to.
  • the lower part of a fining vessel functions as a carrier and holder of molten glass, and thus is in direct contact with the glass.
  • the upper part is reserved for gas to escape and thus is typically free from direct contact with the glass melt during the fining step.
  • the differing heat transfer rate of glass and gas can lead to a non-negligible temperature gradient between the top and the side/bottom of the fining vessel.
  • the temperature of the top portion is measured at the top of the fining vessel.
  • the temperature at this area tends to have the highest temperature of the fining vessel.
  • the temperature of the side portion of the fining vessel is measured at the side of the fining vessel below the melting glass surface line. This area has a temperature very close to that of the glass melt in direct contact therewith.
  • the present inventors have found that maintaining a low temperature gradient between the top and the side/bottom of the fining vessel can allow for a much higher fining temperature of the glass melt, increase the fining efficiency and efficacy, and improve the glass quality.
  • Certain fining systems use direct heating of the fining vessel by passing an electric current through the vessel wall. Certain other fining systems use a separate, indirect and independent heating device, such as metal windings, SiC heating rods, and the like, to heat the fining vessel. Certain other fining systems use a combination of direct and indirect heating means. The present invention can be applied to all these fining systems.
  • DHPS direct-heat platinum fining system
  • FIG. 1 is a schematic illustration of the cross-section of the metal vessel containing molten glass 111 .
  • 103 is the top wall portion of the metal vessel, not in direct contact with molten glass 111 ;
  • 105 is the side wall portion of the vessel, in direct contact with molten glass 111 ;
  • 107 is a first temperature sensor (such as a thermocouple) operable to sense the temperature of the top wall portion;
  • 109 is a second temperature sensor operable to sense the temperature of the side wall portion.
  • FIG. 2 is a schematic illustration of the cross-section of a fining system according to one embodiment of the present invention.
  • 205 is the metal vessel in which molten glass 209 is contained and fined.
  • 201 a , 201 b and 201 c are a first side wall, a base, and a second side wall of a deep cradle containing the vessel 205 .
  • 203 is a bedding material between the cradle walls and the vessel.
  • 207 a and 207 b are cover plates covering the vessel and the bedding material.
  • 211 and 213 are thermal insulating layers enclosing the cradle and the vessel. 213 is advantageously made of fire boards (such as high temperature-resistant fiber boards made of ceramic fiber).
  • the use of a deep cradle in addition to the full insulation of the fining vessel, results in minimal heat loss in the fining process and maintains the temperature gradient of the fining vessel within a desired range.
  • a typical direct heat finer system constructed with high thermal conductivity materials such as alumina insulating firebrick inherently develops a large thermal gradient between the finer top and the tube section below it.
  • the reason for this is that the glass line is lower than the finer top height thus leaving an air space or free glass surface for gas bubbles to escape.
  • the area of the finer top which is not in contact with any glass runs hotter since there is no heat loss into the glass.
  • the maximum glass temperature obtainable is limited by the finer top temperature which is determined by the finer material melting temperature.
  • ⁇ T temperature gradient
  • exemplary approaches to reduce the ⁇ T between the top and bottom of the finer include, but are not limited to: (a) supplemental heating via platinum or KanthalTM windings; (b) insulation package of insulating fire brick and fiberboard; and (c) cooling fins or heat sinks located at the “hot” part of the finer; and (d) alternate top design such as two piece construction or increased thickness, and combinations thereof.
  • active heating or cooling such as in approach (a) and/or (c) it is desired that the heating and/or cooling is controlled by the use of a feedback loop.
  • the temperature gradient between the top and the side portions of the fining vessel are sensed and monitored, and the supplemental heating element, and/or external cooling device, are adjusted and controlled, in conjunction with the direct heating system, if present, to work together to achieve the desired temperature gradient between the top and the side portions.
  • the use of a thicker top portion of the fining vessel can increase the mechanical integrity of the top portion of the fining vessel, even if the top portion is heated to a higher temperature than the side portions. This approach can increase the cost of the fining vessel quite significantly, especially where previous metals, such as Pt and/or Pt—Rh alloys, are employed to construct the high-temperature resistant fining vessel.
  • the preferred embodiment is the use of insulating fire brick and/or fire board as the other methods would require additional energy and power equipment in the case of the windings.
  • the cooling fins or heat sinks could create localized condensation points for PtO 2 , which could generate platinum inclusions.
  • the increased insulation value allows for similar or even higher glass temperatures while using less power.
  • a finer according to the present invention comprising a deep cradle and multiple layers of fire board thermal insulation consumes only about 60-80% of the power required of a comparison finer comprising a less-deep cradle and without multiple layers of fire board thermal insulation.
  • Direct heated platinum systems encompass a voltage across a metal, in certain embodiments, platinum or alloy thereof, which in turn causes the metal to heat up.
  • This method is used to heat the precious metal components of the LCD glass delivery system.
  • the precious metal reaches a significantly higher temperature than the ambient environment or surrounding components.
  • the combination of high temperature and large temperature gradient ( ⁇ T) between platinum and the environment causes an increase in the oxidation rate of the platinum. This situation results in higher oxidation rates than if the precious metal were non-direct heated.
  • the data in FIG. 3 shows that oxidation rates are dependent on the temperature gradient. Shown on the vertical axis of this figure is weight loss (in terms of g ⁇ inch ⁇ 2 ⁇ month ⁇ 1 ) of a Ph-20Rh sample at 1670° C.
  • any approach that can lower the temperature gradient effect may significantly lower oxidation rates of the precious metal.
  • the present invention therefore will reduce the oxidation of the metal vessel wall.

Abstract

A glass making process comprising a step of fining the molten glass in a fining vessel comprising a top wall portion not in direct contact with the molten glass, and a side wall portion in direct contact with the molten glass, wherein the top wall portion has a temperature T(top), the side wall portion has a temperature T(side), and T(top)−T(side)≦10° C., and a glass fining system. The invention is particularly useful for glass fining systems comprising a metal fining vessel made of precious metals such as Pt and/or Pt—Rh alloys.

Description

CROSS-REFERENCE TO RELATED APPLICATION
This application claims the benefit of priority to U.S. provisional application No. 61/002,425, filed on Nov. 8, 2007, the content of which is incorporated herein by reference in its entirety.
TECHNICAL FIELD
The present invention relates to process and system for fining molten glass. In particular, the present invention relates to glass fining process and system comprising a metal fining vessel. The present invention is useful, e.g., in the direct heated platinum fining system for making LCD glass substrate.
BACKGROUND
An exemplary process for manufacturing glass articles begins with the melting of raw feed materials, such as metal oxides, to form a molten glass. The melting process not only results in the formation of glass, but also the formation of various unwanted by-products, including various gases such as oxygen, carbon dioxide, carbon monoxide, sulfur dioxide, sulfur trioxide, argon, nitrogen, and water. Unless removed, these gases can continue throughout the manufacturing process, ending up as small, sometimes microscopic gaseous inclusions or blisters in the finished glass article.
For some glass articles, the presence of small gaseous inclusions is not detrimental. However, for other articles of manufacture, gaseous inclusions as small as 50 μm in diameter are unacceptable. One such article is the glass sheet used in the manufacture of display devices such as liquid crystal and organic light emitting diode displays. For such applications, the glass must have extraordinary clarity, pristine surfaces, and be essentially free of distortion and inclusions.
To remove gaseous inclusions from the molten glass, a fining agent or agents are typically added to the feed material. The fining agent can be a multivalent oxide, such as As2O3. As2O3 is converted into As2O5 during glass melting process. During fining stage, the following reaction occurs:
As2O5→As2O3+O2(gas)
The released oxygen forms gas bubbles in the molten glass, or melt. The gas bubbles allow other dissolved gases to be collected and rise to the surface of the melt, where it is removed from the process. The heating is typically performed in a high temperature fining vessel.
The fining temperatures for display-grade glasses can be as high as 1700° C. Temperatures this high require the use of specialized metals or alloys to prevent destruction of the vessel. Platinum or platinum alloys, such as platinum-rhodium are typically used. Platinum advantageously has a high melting temperature and does not easily dissolve in the glass. Nevertheless, at such high temperatures, the platinum or platinum alloy readily oxidizes. Therefore, steps must be taken to prevent contact between the hot platinum fining vessel and atmospheric oxygen. Other measures for reducing the oxidation of Pt during glass fining and delivery is highly desired as well.
Higher fining temperature of the molten glass is desired in order to obtain higher quality glass for a given residence time in the fining vessel. However, the material forming the fining system such as one made with a metal or a metal alloy, has a maximal operating temperature. Therefore, it would be desirable to have a glass fining system which provides a high fining temperature to the molten glass without exceeding the highest operating temperature of the metal.
The present invention satisfies this need.
SUMMARY
Accordingly, a first aspect of the present invention is a glass making process comprising a step of fining the molten glass in a fining vessel comprising a top wall portion not in direct contact with the molten glass, and a side wall portion in direct contact with the molten glass, wherein the top wall portion has a temperature T(top), the side wall portion has a temperature T(side), and T(top)−T(side)≦10° C.
In certain embodiments of the first aspect of the present invention, T(top)−T(side)≦5° C.
In certain embodiments of the first aspect of the present invention, the wall portions of the vessel comprises a metal.
In certain embodiments of the first aspect of the present invention, the vessel is heated by passing an electric current through the wall portions.
In certain embodiments of the first aspect of the present invention, the wall portions of the vessel comprise Pt.
In certain embodiments of the first aspect of the present invention, T(side)≧1600° C., in certain embodiments T(side)≧1630° C., in certain embodiments T(side)≧1650° C., in certain embodiments T(side)≧1660° C., in certain embodiments T(side)≧1670° C., in certain embodiments T(side)≧1680° C., in certain embodiments T(side)≧1690° C., in certain embodiments T(side)≧1700° C.
In certain embodiments of the first aspect of the present invention, the molten glass is a borosilicate glass, in certain embodiments an aluminoborosilicate glass.
In certain embodiments of the first aspect of the present invention, the fining vessel is supported by a cradle in which the vessel is placed.
In certain embodiments of the first aspect of the present invention, the fining vessel is enclosed by multiple layers of heat-insulating materials.
In certain embodiments of the first aspect of the present invention, the fining vessel is enclosed by at least one layer of heat-insulating material rated for a working temperature of at least 1650° C.
In certain embodiments of the first aspect of the present invention, the fining vessel is enclosed by at least one layer of fire board.
In certain embodiments of the first aspect of the present invention, the side wall portion of the fining vessel is further differentially heated by supplemental heating, such as by passing a current through a Pt heating system or other direct metal heating system.
In certain embodiments of the first aspect of the present invention, cooling fins or heat sinks are installed on the outside of the top wall portion of the fining vessel.
In certain embodiments of the first aspect of the present invention, the top wall portion of the fining vessel has a larger thickness than the side wall portion.
In certain embodiments of the first aspect of the present invention, the wall portions of the fining vessel comprises a metal, and the oxidation of the metal is reduced compared to where T(top)−T(side)≧30° C.
A second aspect of the present invention is a glass fining system comprising:
a metal vessel operable to allow a molten glass to fine therein, having a top wall portion which the molten glass essentially does not directly contact, and a side wall portion which the motel glass directly contact, during a glass fining process;
a first temperature sensor operable to sense the temperature of the top wall portion, and a second temperature sensor operable to sense the temperature of the side wall portion;
a current supply operable to supply an electric current through the wall portions of the metal vessel to heat the top wall portion and the side wall portion of the fining vessel;
a cradle supporting the metal vessel; and
a heat-insulating enclosure containing the metal vessel;
wherein the fining system is operable to maintain a difference between the temperature of the top wall portion, T(top), and the temperature of the side wall portion of the vessel, T(side), during the fining process, wherein T(top)−T(side)≦10° C.
In certain embodiments of the second aspect of the present invention, the system further comprises a heating element operable to differentially heat the side wall portion of the metal vessel, such as a direct Pt heating system or other direct metal heating system.
In certain embodiments of the second aspect of the present invention, a cooling fin or a heat sink is installed on the outside of the top wall portion of the metal vessel.
In certain embodiments of the second aspect of the present invention, the top wall portion of the metal vessel has a higher thickness than the side wall portion.
In certain embodiments of the second aspect of the present invention, the heat-insulating enclosure comprises at least one layer of fire board.
In certain embodiments of the second aspect of the present invention, the metal vessel comprises Pt and/or an alloy thereof.
One or more embodiments of the present invention has one or more of the following advantages: (i) higher quality glass with fewer defects can be produced; (ii) oxidation of metal, such as precious metal, used in the construction of the fining vessel can be reduced, thus extending the life span of the system; (iii) superior thermal insulation of the system can be achieved; and (iv) optimal temperature uniformity of the molten glass can be obtained by using the present invention; (iv) significant capital savings can be realized; and (v) higher select of the glass produced can be obtained.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a schematic illustration of the cross-section of a metal fining vessel used in accordance with one embodiment of the present invention.
FIG. 2 is a schematic illustration of the cross-section of a fining system according to one embodiment of the present invention.
FIG. 3 is a diagram showing the oxidation (indicated by weight loss) of Pt—Rh alloy at various temperature and temperature gradient.
 DETAILED DESCRIPTION
Unless otherwise indicated, all numbers such as those expressing weight percents of ingredients, dimensions, and values for certain physical properties used in the specification and claims are to be understood as being modified in all instances by the term “about.” It should also be understood that the precise numerical values used in the specification and claims form additional embodiments of the invention. Efforts have been made to ensure the accuracy of the numerical values disclosed in the Examples. Any measured numerical value, however, can inherently contain certain errors resulting from the standard deviation found in its respective measuring technique.
As used herein, in describing and claiming the present invention, the use of the indefinite article “a” or “an” means “at least one,” and should not be limited to “only one” unless explicitly indicated to the contrary. Thus, for example, reference to “a fining vessel” includes embodiments having two or more fining vessels, unless the context clearly indicates otherwise.
A typical glass fining system comprises a fining vessel where molten glass is contained for a certain period of residence time, where gas bubbles inside the molten glass are allowed to rise from inside the molten glass to the surface. All other conditions being equal, the lower the viscosity of the molten glass, the easier it is for the bubbles to form and rise in the melt. It is desirable that the molten glass in the fining vessel is heated to a sufficiently high temperature to allow for a sufficiently low glass viscosity. The highest temperature the glass melt can reach is determined in part by the material of the fining vessel. Take a fining system comprising a Pt fining vessel as an example. The temperature of the molten glass cannot exceed the melting temperature of Pt. Pure Pt has a melting point of 1768° C. The mechanical integrity of the Pt fining vessel can be seriously compromised if it is heated to a temperature close to its melting point.
As mentioned above, differing parts of the fining vessel of a fining system may be subjected to differential heating during a fining process, due in part to the differing environment they are exposed to. The lower part of a fining vessel functions as a carrier and holder of molten glass, and thus is in direct contact with the glass. However, the upper part is reserved for gas to escape and thus is typically free from direct contact with the glass melt during the fining step. The differing heat transfer rate of glass and gas can lead to a non-negligible temperature gradient between the top and the side/bottom of the fining vessel. In the present application, the temperature of the top portion is measured at the top of the fining vessel. The temperature at this area tends to have the highest temperature of the fining vessel. The temperature of the side portion of the fining vessel is measured at the side of the fining vessel below the melting glass surface line. This area has a temperature very close to that of the glass melt in direct contact therewith.
The present inventors have found that maintaining a low temperature gradient between the top and the side/bottom of the fining vessel can allow for a much higher fining temperature of the glass melt, increase the fining efficiency and efficacy, and improve the glass quality.
In addition, it has been found that, by reducing the temperature gradient between the top and the side/bottom of the fining vessel, oxidation of the metal can be reduced, thereby extending service life of the fining system.
Certain fining systems use direct heating of the fining vessel by passing an electric current through the vessel wall. Certain other fining systems use a separate, indirect and independent heating device, such as metal windings, SiC heating rods, and the like, to heat the fining vessel. Certain other fining systems use a combination of direct and indirect heating means. The present invention can be applied to all these fining systems.
The present invention is illustrated below in the context of a direct-heat platinum fining system (DHPS). It is to be noted that DHPS is merely one embodiment of the present invention, and the present invention may be implemented in other glass making systems as well.
FIG. 1 is a schematic illustration of the cross-section of the metal vessel containing molten glass 111. 103 is the top wall portion of the metal vessel, not in direct contact with molten glass 111; 105 is the side wall portion of the vessel, in direct contact with molten glass 111; 107 is a first temperature sensor (such as a thermocouple) operable to sense the temperature of the top wall portion; and 109 is a second temperature sensor operable to sense the temperature of the side wall portion. By use of the two temperature sensors, the temperature gradient between the top and side/bottom portions of the fining vessels are monitored. In the case of a DHPS, electric currents fed into the fining vessel can be modulated and adjusted accordingly, so that the top portion and the side/bottom portions are heated differentially to maintain the temperature gradient within desired range.
FIG. 2 is a schematic illustration of the cross-section of a fining system according to one embodiment of the present invention. 205 is the metal vessel in which molten glass 209 is contained and fined. 201 a, 201 b and 201 c are a first side wall, a base, and a second side wall of a deep cradle containing the vessel 205. 203 is a bedding material between the cradle walls and the vessel. 207 a and 207 b are cover plates covering the vessel and the bedding material. 211 and 213 are thermal insulating layers enclosing the cradle and the vessel. 213 is advantageously made of fire boards (such as high temperature-resistant fiber boards made of ceramic fiber). In this embodiment, the use of a deep cradle, in addition to the full insulation of the fining vessel, results in minimal heat loss in the fining process and maintains the temperature gradient of the fining vessel within a desired range.
A typical direct heat finer system constructed with high thermal conductivity materials such as alumina insulating firebrick inherently develops a large thermal gradient between the finer top and the tube section below it. The reason for this is that the glass line is lower than the finer top height thus leaving an air space or free glass surface for gas bubbles to escape. The area of the finer top which is not in contact with any glass runs hotter since there is no heat loss into the glass. As a result the maximum glass temperature obtainable is limited by the finer top temperature which is determined by the finer material melting temperature. The larger the temperature gradient (ΔT), the lower the glass temperature and the fining capabilities are reduced.
Various approaches can be used to reduce the temperature gradient (ΔT) between the top portion and the side portions of the fining vessel. Exemplary approaches to reduce the ΔT between the top and bottom of the finer include, but are not limited to: (a) supplemental heating via platinum or Kanthal™ windings; (b) insulation package of insulating fire brick and fiberboard; and (c) cooling fins or heat sinks located at the “hot” part of the finer; and (d) alternate top design such as two piece construction or increased thickness, and combinations thereof. In certain embodiments, where active heating or cooling is utilized, such as in approach (a) and/or (c), it is desired that the heating and/or cooling is controlled by the use of a feedback loop. Thus, the temperature gradient between the top and the side portions of the fining vessel are sensed and monitored, and the supplemental heating element, and/or external cooling device, are adjusted and controlled, in conjunction with the direct heating system, if present, to work together to achieve the desired temperature gradient between the top and the side portions. The use of a thicker top portion of the fining vessel can increase the mechanical integrity of the top portion of the fining vessel, even if the top portion is heated to a higher temperature than the side portions. This approach can increase the cost of the fining vessel quite significantly, especially where previous metals, such as Pt and/or Pt—Rh alloys, are employed to construct the high-temperature resistant fining vessel.
The preferred embodiment is the use of insulating fire brick and/or fire board as the other methods would require additional energy and power equipment in the case of the windings. The cooling fins or heat sinks could create localized condensation points for PtO2, which could generate platinum inclusions. In addition, the increased insulation value allows for similar or even higher glass temperatures while using less power.
Ability to Raise Glass Temperature to Improve Fining Capability
Data have shown a fining system according to the present invention utilizing multiple layers of fire boards for thermal insulating cradles achieved a T(top)−T(side)≈10° C. Whereas in a comparative finer having essentially the same dimension and geometry without sufficient thermal insulation of the fining vessel, a temperature difference of T(top)−T(side)≈40° C. was observed.
Data showed that power consumption of the fining system of the present invention is significantly lower. A finer according to the present invention comprising a deep cradle and multiple layers of fire board thermal insulation consumes only about 60-80% of the power required of a comparison finer comprising a less-deep cradle and without multiple layers of fire board thermal insulation.
Quality of the glass fined by using the fining system according to the present invention was significantly higher than glass fined by using comparison fining system. Glass fined by using comparison finers comprised about 1.7˜6 times blisters of the glass fined according to the present invention. Without intending to be bound by any particular theory, it is believed this is due to the higher temperature of the molten glass achieved in the finer.
Total loss of glass therefore is much lower for the present invention.
Reduction of Precious Metal Oxidation to Control Glass Leaks Via Low Thermal Conductivity Insulation
Direct heated platinum systems encompass a voltage across a metal, in certain embodiments, platinum or alloy thereof, which in turn causes the metal to heat up. This method is used to heat the precious metal components of the LCD glass delivery system. As a result, the precious metal reaches a significantly higher temperature than the ambient environment or surrounding components. The combination of high temperature and large temperature gradient (ΔT) between platinum and the environment causes an increase in the oxidation rate of the platinum. This situation results in higher oxidation rates than if the precious metal were non-direct heated. The data in FIG. 3 shows that oxidation rates are dependent on the temperature gradient. Shown on the vertical axis of this figure is weight loss (in terms of g·inch−2·month−1) of a Ph-20Rh sample at 1670° C. Shown on the horizontal axis is the ambient temperature the test Pt-20Rh plate was subjected to. Therefore, any approach that can lower the temperature gradient effect may significantly lower oxidation rates of the precious metal. The present invention therefore will reduce the oxidation of the metal vessel wall.
The use of a better insulating package is going to reduce the amount of power necessary for optimal operation, which means that the platinum surface, especially in the top wall portion, can run at a lower temperature. Lower power means a lower oxidation rate, which implies the precious metal will maintain its integrity longer. Consequently, for direct heat components such as a glass finer, the time to failure due to glass leaks or structural weakness will occur later.
It will be apparent to those skilled in the art that various modifications and alterations can be made to the present invention without departing from the scope and spirit of the invention. Thus, it is intended that the present invention cover the modifications and variations of this invention provided they come within the scope of the appended claims and their equivalents.

Claims (23)

What is claimed is:
1. A glass making process comprising the steps of:
fining molten glass in a fining vessel comprising a top wall portion not in direct contact with the molten glass, and a side wall portion in direct contact with the molten glass, wherein the top wall portion has a temperature T(top), the side wall portion has a temperature T(side); and
reducing a temperature gradient between the top wall portion and the side wall portion such that T(top)−T(side)≦10° C.
2. A glass making process according to claim 1, wherein T(top)>T(side).
3. A glass making process according to claim 2, wherein T(top)−T(side)≧5° C.
4. A glass making process according to claim 1, wherein the wall portions of the vessel comprises a metal.
5. A glass making process according to claim 4, wherein the vessel is heated by passing an electric current through the wall portions.
6. A glass making process according to claim 1, wherein the wall portions of the vessel comprises Pt.
7. A glass making process according to claim 1, wherein the T(side)≧1600° C.
8. A glass making process according to claim 1, wherein the molten glass is a borosilicate glass.
9. A glass making process according to claim 1, wherein the step of reducing the temperature gradient includes supporting the fining vessel by a cradle.
10. A glass making process according to claim 1, wherein the step of reducing the temperature gradient includes enclosing the fining vessel with multiple layers of heat-insulating materials.
11. A glass making process according to claim 10, wherein the multiple layers of heat-insulating materials includes at least one layer of heat-insulating material rated for 1650° C. working temperature.
12. A glass making process according to claim 1, wherein the step of reducing the temperature gradient includes enclosing the fining vessel with at least one layer of fire board.
13. A glass making process according to claim 1, wherein the step of reducing the temperature gradient includes differentially heating the side wall portion of the vessel by supplemental heating.
14. A glass making process according to claim 13, wherein the supplemental heating is provided by passing a current through a direct metal heating system.
15. A glass making process according to claim 1, wherein the step of reducing the temperature gradient includes installing a heat sink on the outside of the top wall portion of the fining vessel.
16. A glass making process according to claim 15, wherein the heat sink comprises cooling fins.
17. A glass making process according to claim 1, wherein the step of reducing the temperature gradient includes providing the top wall portion of the fining vessel with a larger thickness than the side wall portion.
18. A glass making process according to claim 1, wherein the wall portions of the fining vessel comprises a metal, and the oxidation of the metal is reduced compared to where T(top)−T(side)≧30° C.
19. A glass making process comprising the steps of:
fining molten glass in a fining vessel comprising a top wall portion not in direct contact with the molten glass, and a side wall portion in direct contact with the molten glass, wherein the top wall portion has a temperature T(top), the side wall portion has a temperature T(side); and
increasing a maximum temperature of the molten glass within the fining vessel by reducing a temperature gradient between the top wall portion and the side wall portion such that T(top)−T(side)≦10° C.
20. A glass making process according to claim 19, wherein the step of reducing the temperature gradient includes supporting the fining vessel by a cradle.
21. A glass making process according to claim 19, wherein the step of reducing the temperature gradient includes enclosing the fining vessel with multiple layers of heat-insulating materials.
22. A glass making process according to claim 21, wherein the multiple layers of heat-insulating materials includes at least one layer of heat-insulating material rated for 1650° C. working temperature.
23. A glass making process according to claim 19, wherein the step of reducing the temperature gradient includes enclosing the fining vessel with at least one layer of fire board.
US12/264,562 2007-11-08 2008-11-04 Process and system for fining glass Active 2032-08-23 US8925353B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US12/264,562 US8925353B2 (en) 2007-11-08 2008-11-04 Process and system for fining glass

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US242507P 2007-11-08 2007-11-08
US12/264,562 US8925353B2 (en) 2007-11-08 2008-11-04 Process and system for fining glass

Publications (2)

Publication Number Publication Date
US20090120133A1 US20090120133A1 (en) 2009-05-14
US8925353B2 true US8925353B2 (en) 2015-01-06

Family

ID=40361427

Family Applications (1)

Application Number Title Priority Date Filing Date
US12/264,562 Active 2032-08-23 US8925353B2 (en) 2007-11-08 2008-11-04 Process and system for fining glass

Country Status (6)

Country Link
US (1) US8925353B2 (en)
JP (4) JP2011502934A (en)
KR (2) KR101658898B1 (en)
CN (1) CN101932530B (en)
TW (1) TWI410386B (en)
WO (1) WO2009061484A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11919800B2 (en) 2018-09-27 2024-03-05 Corning Incorporated Modular molten glass delivery apparatus

Families Citing this family (42)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090272150A1 (en) * 2007-11-02 2009-11-05 Lawrence Henry Kotacska Corrosion-resistant cradle and castable materials for glass production
US10322960B2 (en) 2010-06-17 2019-06-18 Johns Manville Controlling foam in apparatus downstream of a melter by adjustment of alkali oxide content in the melter
US9032760B2 (en) 2012-07-03 2015-05-19 Johns Manville Process of using a submerged combustion melter to produce hollow glass fiber or solid glass fiber having entrained bubbles, and burners and systems to make such fibers
US9096453B2 (en) * 2012-06-11 2015-08-04 Johns Manville Submerged combustion melting processes for producing glass and similar materials, and systems for carrying out such processes
US8707740B2 (en) 2011-10-07 2014-04-29 Johns Manville Submerged combustion glass manufacturing systems and methods
US8997525B2 (en) 2010-06-17 2015-04-07 Johns Manville Systems and methods for making foamed glass using submerged combustion
US9021838B2 (en) 2010-06-17 2015-05-05 Johns Manville Systems and methods for glass manufacturing
KR101305612B1 (en) * 2010-09-30 2013-09-09 아반스트레이트 가부시키가이샤 Method for producing glass sheet
DE102010047896B4 (en) * 2010-10-11 2016-03-03 Heraeus Deutschland GmbH & Co. KG Reduction of the evaporation rate from platinum and Pt alloys: component and process
US20130025323A1 (en) * 2011-07-25 2013-01-31 Lineman David M Fiber-based gasket, glass manufacturing system, and method for reducing thermal cell induced blisters
JP5769574B2 (en) * 2011-09-30 2015-08-26 ＡｖａｎＳｔｒａｔｅ株式会社 Manufacturing method of glass plate
CN103476716B (en) * 2012-04-05 2016-11-02 安瀚视特控股株式会社 The manufacture method of glass substrate and glass substrate manufacture device
US9533905B2 (en) 2012-10-03 2017-01-03 Johns Manville Submerged combustion melters having an extended treatment zone and methods of producing molten glass
CN103508654B (en) * 2012-06-29 2016-08-03 安瀚视特控股株式会社 The manufacture method of glass substrate and the manufacture device of glass substrate
JP5824433B2 (en) * 2012-08-29 2015-11-25 ＡｖａｎＳｔｒａｔｅ株式会社 Glass plate manufacturing method and glass plate manufacturing apparatus
CN203498243U (en) * 2012-09-27 2014-03-26 安瀚视特控股株式会社 Glass substrate making device
EP2903941A4 (en) 2012-10-03 2016-06-08 Johns Manville Methods and systems for destabilizing foam in equipment downstream of a submerged combustion melter
US20140123710A1 (en) * 2012-11-02 2014-05-08 David Myron Lineman Apparatus and method for minimizing platinum group metal particulate inclusion in molten glass
US9227865B2 (en) 2012-11-29 2016-01-05 Johns Manville Methods and systems for making well-fined glass using submerged combustion
KR101716996B1 (en) * 2013-02-01 2017-03-15 아반스트레이트 가부시키가이샤 Method for manufacturing glass substrate and glass substrate manufacturing apparatus
CN110803857B (en) * 2013-10-18 2022-01-25 康宁股份有限公司 Apparatus and method for making glass
WO2015099157A1 (en) * 2013-12-26 2015-07-02 ＡｖａｎＳｔｒａｔｅ株式会社 Method for producing glass substrate and glass-substrate production device
WO2015099136A1 (en) * 2013-12-26 2015-07-02 ＡｖａｎＳｔｒａｔｅ株式会社 Manufacturing method for glass substrate and manufacturing apparatus for glass substrate
TWI568696B (en) * 2013-12-26 2017-02-01 Avanstrate Inc A glass substrate manufacturing method and a glass substrate manufacturing apparatus
JP6247958B2 (en) * 2014-02-26 2017-12-13 ＡｖａｎＳｔｒａｔｅ株式会社 Glass plate manufacturing method and glass plate manufacturing apparatus
CN204356216U (en) * 2014-03-31 2015-05-27 安瀚视特控股株式会社 Glass substrate manufacturing installation
WO2016002814A1 (en) * 2014-06-30 2016-01-07 ＡｖａｎＳｔｒａｔｅ株式会社 Glass substrate manufacturing method, glass substrate, and glass substrate layered body
US9751792B2 (en) 2015-08-12 2017-09-05 Johns Manville Post-manufacturing processes for submerged combustion burner
US10670261B2 (en) 2015-08-27 2020-06-02 Johns Manville Burner panels, submerged combustion melters, and methods
US10041666B2 (en) 2015-08-27 2018-08-07 Johns Manville Burner panels including dry-tip burners, submerged combustion melters, and methods
US9815726B2 (en) 2015-09-03 2017-11-14 Johns Manville Apparatus, systems, and methods for pre-heating feedstock to a melter using melter exhaust
US9982884B2 (en) 2015-09-15 2018-05-29 Johns Manville Methods of melting feedstock using a submerged combustion melter
US10837705B2 (en) 2015-09-16 2020-11-17 Johns Manville Change-out system for submerged combustion melting burner
US10081563B2 (en) 2015-09-23 2018-09-25 Johns Manville Systems and methods for mechanically binding loose scrap
US10144666B2 (en) 2015-10-20 2018-12-04 Johns Manville Processing organics and inorganics in a submerged combustion melter
US10246362B2 (en) 2016-06-22 2019-04-02 Johns Manville Effective discharge of exhaust from submerged combustion melters and methods
US10301208B2 (en) 2016-08-25 2019-05-28 Johns Manville Continuous flow submerged combustion melter cooling wall panels, submerged combustion melters, and methods of using same
US10196294B2 (en) 2016-09-07 2019-02-05 Johns Manville Submerged combustion melters, wall structures or panels of same, and methods of using same
US10233105B2 (en) 2016-10-14 2019-03-19 Johns Manville Submerged combustion melters and methods of feeding particulate material into such melters
US20210032148A1 (en) * 2017-12-01 2021-02-04 Corning Incorporated Apparatus and method for producing glass
KR20210064347A (en) * 2018-09-27 2021-06-02 코닝 인코포레이티드 Glass forming apparatuses including modular glass clarification systems
US20200140327A1 (en) * 2018-11-01 2020-05-07 Corning Incorporated Strengthened glass articles with reduced delayed breakage and methods of making the same

Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3708271A (en) * 1970-12-07 1973-01-02 Oliver Glass Fiber Corp Apparatus for producing glass fibers
US3777040A (en) 1973-04-25 1973-12-04 Toledo Eng Co Inc Protection of glass melting furnace electrode
US4494974A (en) * 1981-10-19 1985-01-22 B.H.F. (Engineering) Ltd. Forehearth for conditioning glass
US4622678A (en) * 1984-07-05 1986-11-11 Electroglass Limited Electrically heated forehearth
US4780122A (en) 1987-06-29 1988-10-25 Ppg Industries, Inc. Vacuum refining of glass or the like with enhanced foaming
JPS63310734A (en) 1987-05-30 1988-12-19 ベタイリグンゲン・ゾルク・ゲー・エム・ベー・ハー・ウント・コー・カー・ゲー Glass melting process and furnace
US4906272A (en) 1989-04-17 1990-03-06 Corning Incorporated Furnace for fining molten glass
US6286337B1 (en) 2000-06-29 2001-09-11 Corning Incorporated Tubing system for reduced pressure finer
US20040067369A1 (en) * 2000-11-30 2004-04-08 Franz Ott Coated metal element used for producing glass
US6769272B2 (en) 2000-02-28 2004-08-03 Schott Glas Method and apparatus for oxygen refinement of a glass melt
US20040177649A1 (en) 2003-03-13 2004-09-16 Corning Incorporated Methods of manufacturing glass sheets with reduced blisters
US6848275B1 (en) * 1999-08-21 2005-02-01 Schott Glas Method for melting or refining glasses or glass ceramics
JP2005119958A (en) 2003-10-13 2005-05-12 Schott Ag Glass molten body refining apparatus
US20050155387A1 (en) * 2001-07-18 2005-07-21 Hayes James C. Method for controlling foam production in reduced pressure fining
US20060242995A1 (en) * 2005-04-27 2006-11-02 Bookbinder Andrea W Method of fining glass
US20060242996A1 (en) * 2005-04-27 2006-11-02 Gilbert Deangelis System and method for controlling the environment around one or more vessels in a glass manufacturing system
WO2008108943A1 (en) 2007-03-01 2008-09-12 Corning Incorporated Apparatus for fining glass

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4932035A (en) * 1987-05-30 1990-06-05 Sorg Gmbh & Co. Kg Discontinuous glass melting furnace
JP3530666B2 (en) * 1995-03-07 2004-05-24 キヤノン株式会社 Equipment for manufacturing molten glass raw materials
DE19939771B4 (en) * 1999-08-21 2004-04-15 Schott Glas Process for refining glass melts
DE10041757C1 (en) * 2000-08-25 2002-02-21 Schott Glas Method and device for refining glass
CN100467409C (en) * 2002-12-27 2009-03-11 旭硝子株式会社 Conduit for molten glass, molten glass degassing method and molten glass degassing apparatus
JP2005047768A (en) * 2003-07-31 2005-02-24 Asahi Glass Co Ltd Operation support system for glass melting vessel
JP2006219371A (en) * 2006-04-26 2006-08-24 Asahi Glass Co Ltd Vacuum degassing apparatus for molten glass and its manufacturing method

Patent Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3708271A (en) * 1970-12-07 1973-01-02 Oliver Glass Fiber Corp Apparatus for producing glass fibers
US3777040A (en) 1973-04-25 1973-12-04 Toledo Eng Co Inc Protection of glass melting furnace electrode
US4494974A (en) * 1981-10-19 1985-01-22 B.H.F. (Engineering) Ltd. Forehearth for conditioning glass
US4622678A (en) * 1984-07-05 1986-11-11 Electroglass Limited Electrically heated forehearth
JPS63310734A (en) 1987-05-30 1988-12-19 ベタイリグンゲン・ゾルク・ゲー・エム・ベー・ハー・ウント・コー・カー・ゲー Glass melting process and furnace
US4882736A (en) 1987-05-30 1989-11-21 Sorg Gmbh & Co. Kg Method for efficiently using flue gas energy in a glass furnace
US4780122A (en) 1987-06-29 1988-10-25 Ppg Industries, Inc. Vacuum refining of glass or the like with enhanced foaming
JPS6418926A (en) 1987-06-29 1989-01-23 Ppg Industries Inc Vacuum purification of glass or like by increased foaming
US4906272A (en) 1989-04-17 1990-03-06 Corning Incorporated Furnace for fining molten glass
US4906272B1 (en) 1989-04-17 1992-09-15 Corning Glass Works
US6848275B1 (en) * 1999-08-21 2005-02-01 Schott Glas Method for melting or refining glasses or glass ceramics
US6769272B2 (en) 2000-02-28 2004-08-03 Schott Glas Method and apparatus for oxygen refinement of a glass melt
US6286337B1 (en) 2000-06-29 2001-09-11 Corning Incorporated Tubing system for reduced pressure finer
US20040067369A1 (en) * 2000-11-30 2004-04-08 Franz Ott Coated metal element used for producing glass
US20050155387A1 (en) * 2001-07-18 2005-07-21 Hayes James C. Method for controlling foam production in reduced pressure fining
US20040177649A1 (en) 2003-03-13 2004-09-16 Corning Incorporated Methods of manufacturing glass sheets with reduced blisters
JP2005119958A (en) 2003-10-13 2005-05-12 Schott Ag Glass molten body refining apparatus
US20060242995A1 (en) * 2005-04-27 2006-11-02 Bookbinder Andrea W Method of fining glass
US20060242996A1 (en) * 2005-04-27 2006-11-02 Gilbert Deangelis System and method for controlling the environment around one or more vessels in a glass manufacturing system
WO2008108943A1 (en) 2007-03-01 2008-09-12 Corning Incorporated Apparatus for fining glass

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Biser, Benjamin Franklin, Elements of glass and glass making. Glass and Pottery Publishing Company, Pittsburgh, PA. 1899, p. 54. *
Rathke, Sicco, Advances in Direct Heated Platinum Coatings for Glass Manufacture, Handbuch Der Glastechnik: Production, Properties and Applications of Refractory and Platinum Group Metals for the Contract with Glass Melts:: H üttentechnische Vereingigung Der Deutschen Glasindustrie, 2006, pp. 77-90, XP002517046 p. 85, line 1-p. 86, line 9.

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11919800B2 (en) 2018-09-27 2024-03-05 Corning Incorporated Modular molten glass delivery apparatus

Also Published As

Publication number Publication date
KR20150126711A (en) 2015-11-12
WO2009061484A1 (en) 2009-05-14
TW200946470A (en) 2009-11-16
KR101658898B1 (en) 2016-09-22
JP2015214486A (en) 2015-12-03
CN101932530A (en) 2010-12-29
CN101932530B (en) 2013-09-04
US20090120133A1 (en) 2009-05-14
TWI410386B (en) 2013-10-01
JP2011502934A (en) 2011-01-27
JP2017100941A (en) 2017-06-08
JP2014148459A (en) 2014-08-21
KR20100119537A (en) 2010-11-09

Similar Documents

Publication Publication Date Title
US8925353B2 (en) Process and system for fining glass
KR102110322B1 (en) Apparatus for use in direct resistance heating of platinum-containing vessels
US20090165500A1 (en) Method and Device for Bubble-free Transportation, Homogenization and Conditioning of Molten Glass
KR20080095241A (en) Device and method for the continuous fining of gasses with high purity requirements
JP2006516046A (en) Melt heating method and apparatus
JP5122855B2 (en) Glass fiber production equipment
US10656024B2 (en) Molten material thermocouple methods and apparatus
KR101454049B1 (en) Apparatus for fining glass
US11505487B2 (en) Method for decreasing bubble lifetime on a glass melt surface
WO2006085552A1 (en) Float bath and float forming method
JPWO2013150912A1 (en) Glass substrate manufacturing method and glass substrate manufacturing apparatus
JP7341999B2 (en) Apparatus and method for producing glass
JP2017066016A (en) Method and apparatus for manufacturing float plate glass
JP2014069983A (en) Method and apparatus for producing glass substrate
JP2008094644A (en) Method for producing glass and glass molding device
JP6630217B2 (en) Manufacturing method of glass plate
JP6070576B2 (en) Sheet glass manufacturing apparatus and sheet glass manufacturing method
JP2008064387A (en) Heating furnace and heating method for heating object
JP2017065960A (en) Method of manufacturing glass substrate

Legal Events

Date Code Title Description
AS Assignment

Owner name: CORNING INCORPORATED, NEW YORK

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:FRALEY, RAYMOND EUGENE;GRZESIK, PAUL RICHARD;KOTACSKA, LAWRENCE HENRY;AND OTHERS;REEL/FRAME:021830/0559;SIGNING DATES FROM 20081017 TO 20081112

Owner name: CORNING INCORPORATED, NEW YORK

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:FRALEY, RAYMOND EUGENE;GRZESIK, PAUL RICHARD;KOTACSKA, LAWRENCE HENRY;AND OTHERS;SIGNING DATES FROM 20081017 TO 20081112;REEL/FRAME:021830/0559

STCF Information on status: patent grant

Free format text: PATENTED CASE

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 4TH YEAR, LARGE ENTITY (ORIGINAL EVENT CODE: M1551)

Year of fee payment: 4

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 8TH YEAR, LARGE ENTITY (ORIGINAL EVENT CODE: M1552); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Year of fee payment: 8